CN103542706A - Drying system of organoboron production - Google Patents
Drying system of organoboron production Download PDFInfo
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- CN103542706A CN103542706A CN201210244125.XA CN201210244125A CN103542706A CN 103542706 A CN103542706 A CN 103542706A CN 201210244125 A CN201210244125 A CN 201210244125A CN 103542706 A CN103542706 A CN 103542706A
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- dust removal
- removal device
- stage dust
- drying
- drying system
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Abstract
The invention relates to a drying system of organoboron production. The drying system comprises an air feeder, a centrifugal atomizer, a drying tower, a first-grade dust removal device, a second-stage dust removal device, a backflow fan, an air dehumidifier, a clone separator and a stock bin. The centrifugal atomizer is connected with a feeding system, the position below an outlet of the centrifugal atomizer is right opposite to an inlet of the drying tower, the air feeder is connected with the inlet of the drying tower, an outlet of the drying tower is connected with the first-stage dust removal device, a material pumping device is installed on the first-stage dust removal device and connected to the second-stage dust removal device, the second-stage dust removal device is connected with the clone separator through the backflow fan, an outlet of the clone separator is connected with the stock bin, and a leading-out pipe of the air dehumidifier is respectively connected with the first-stage dust removal device, the second-stage dust removal device and the clone separator. According to the drying system, automatic-control, continuous and large-scale production is adopted, the production cost is reduced, manpower is saved, the drying and dehumidification effects are good, and the product quality is improved.
Description
Technical field
The invention belongs to chemical industry preparing technical field, particularly relate to a kind of drying system of producing organic boron.
Background technology
At present, in the manufacture of organic boron, have following shortcoming, drying means can not serialization, scale, industrialization; Dry and effect on moisture extraction is not very desirable.Therefore, urgently person skilled in art's developmental research goes out a kind of more satisfactory drying system.
Summary of the invention
Object of the present invention is exactly to provide a kind of drying system of producing organic boron for above-mentioned the deficiencies in the prior art part, thereby realizes automation, serialization production, and has good dry, effect on moisture extraction, can overcome the problem of above-mentioned prior art completely.
The object of the invention is to realize in the following way: a kind of drying system of producing organic boron, comprise pressure fan, centrifugal atomizer, drying tower, primary dust removing device, two-stage dust removal device, backflow blower fan, airdryer, cyclone separator and feed bin, centrifugal atomizer is connected with feed system, its outlet below is over against drying tower entrance, pressure fan is connected with drying tower entrance, drying tower outlet is connected with primary dust removing device, on primary dust removing device, install and take out glassware and be connected to two-stage dust removal device, secondary ash collector is connected with cyclone separator by backflow blower fan, cyclone separator outlet connects feed bin, airdryer pick out pipeline respectively with primary dust removing device, two-stage dust removal device is connected with cyclone separator.
Further, the mouth of pipe place that primary dust removing device is connected with airdryer with two-stage dust removal device is provided with rotary valve.
Further, two-stage dust removal device also connects an air-introduced machine.
Further, described two-stage dust removal device is sack cleaner.
Further, described feed bin is bevel-type feed bin.
Compared with prior art, beneficial effect of the present invention is: adopt control automatically, serialization, large-scale production, reduced production cost, saved manpower, dry good with effect on moisture extraction, product quality is improved.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
The specific embodiment
Below in conjunction with drawings and the specific embodiments, the present invention is described in further detail.
As shown in Figure 1, a kind of drying system of producing organic boron, comprise pressure fan 11, centrifugal atomizer 1, drying tower 2, primary dust removing device 3, sack cleaner 4, backflow blower fan 5, airdryer 13, cyclone separator 6 and bevel-type feed bin 7, centrifugal atomizer 1 is connected with feed system 12, its outlet below is over against drying tower 2 entrances, pressure fan 11 is connected with drying tower 2 entrances, drying tower 2 outlets are connected with primary dust removing device 3, on primary dust removing device 3, install and take out glassware 9 and be connected to sack cleaner 4, sack cleaner 4 is connected with cyclone separator 6 by backflow blower fan 5, cyclone separator 6 outlets connect bevel-type feed bin 7, airdryer 13 pick out pipeline respectively with primary dust removing device 3, sack cleaner 4 is connected with cyclone separator 6.
Primary dust removing device 3 is provided with rotary valve 10 with the mouth of pipe place that sack cleaner 4 is connected with airdryer 13.
Sack cleaner 4 also connects an air-introduced machine 8.
When work, feed system 12 carries semi-finished product organic boron to enter drying tower 2 through centrifugal atomizer 1, pressure fan 11 is sent coal gas and air into drying tower 2, after organic boron is dry, enter primary dust removing device 3 and sack cleaner 4 dedustings, airdryer 13 and 5 work of backflow blower fan simultaneously dehumidify, and last organic boron enters bevel-type feed bin 7 through cyclone separator 6 and obtains finished product organic boron.
The foregoing is only preferred embodiment of the present invention, not in order to limit the present invention, all any modifications of doing within the spirit and principles in the present invention, be equal to and replace and improvement etc., within all should being included in protection scope of the present invention.
Claims (5)
1. a drying system of producing organic boron, it is characterized in that: comprise pressure fan, centrifugal atomizer, drying tower, primary dust removing device, two-stage dust removal device, backflow blower fan, airdryer, cyclone separator and feed bin, centrifugal atomizer is connected with feed system, its outlet below is over against drying tower entrance, pressure fan is connected with drying tower entrance, drying tower outlet is connected with primary dust removing device, on primary dust removing device, install and take out glassware and be connected to two-stage dust removal device, secondary ash collector is connected with cyclone separator by backflow blower fan, cyclone separator outlet connects feed bin, airdryer pick out pipeline respectively with primary dust removing device, two-stage dust removal device is connected with cyclone separator.
2. the drying system of production organic boron according to claim 1, is characterized in that: the mouth of pipe place that primary dust removing device is connected with airdryer with two-stage dust removal device is provided with rotary valve.
3. the drying system of production organic boron according to claim 1, is characterized in that: two-stage dust removal device also connects an air-introduced machine.
4. the drying system of production organic boron according to claim 1, is characterized in that: described two-stage dust removal device is sack cleaner.
5. the drying system of production organic boron according to claim 1, is characterized in that: described feed bin is bevel-type feed bin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210244125.XA CN103542706A (en) | 2012-07-16 | 2012-07-16 | Drying system of organoboron production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210244125.XA CN103542706A (en) | 2012-07-16 | 2012-07-16 | Drying system of organoboron production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103542706A true CN103542706A (en) | 2014-01-29 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210244125.XA Pending CN103542706A (en) | 2012-07-16 | 2012-07-16 | Drying system of organoboron production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103542706A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107875661A (en) * | 2017-12-25 | 2018-04-06 | 无锡市尚德干燥设备有限公司 | Multilevel drying machine |
Citations (7)
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| US5695614A (en) * | 1991-03-21 | 1997-12-09 | Winter Umwelttechinik Gmbh | Method for processing waste liquids in particular industrial waste water having a high solids content |
| CN2475979Y (en) * | 2001-03-27 | 2002-02-06 | 常州市第二干燥设备厂 | Lauryl alcohol (foaming agent) spraying-drying cooling tower |
| CN2816709Y (en) * | 2005-05-30 | 2006-09-13 | 查国才 | Loop-circulation centrifugal atemizing dryer |
| CN1965704A (en) * | 2005-11-16 | 2007-05-23 | 北京宝得瑞食品有限公司 | Preparation method of seabuckthorn fruit powder and production equipment thereof |
| CN101178283A (en) * | 2006-11-06 | 2008-05-14 | 谢洪清 | Seasoner sponging drying machine group |
| CN201551860U (en) * | 2009-11-23 | 2010-08-18 | 陆文光 | Centrifugal spray dryer unit |
| CN102374759A (en) * | 2010-08-11 | 2012-03-14 | 焦作健康元生物制品有限公司 | Mushroom scrap spray-drying system |
-
2012
- 2012-07-16 CN CN201210244125.XA patent/CN103542706A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5695614A (en) * | 1991-03-21 | 1997-12-09 | Winter Umwelttechinik Gmbh | Method for processing waste liquids in particular industrial waste water having a high solids content |
| CN2475979Y (en) * | 2001-03-27 | 2002-02-06 | 常州市第二干燥设备厂 | Lauryl alcohol (foaming agent) spraying-drying cooling tower |
| CN2816709Y (en) * | 2005-05-30 | 2006-09-13 | 查国才 | Loop-circulation centrifugal atemizing dryer |
| CN1965704A (en) * | 2005-11-16 | 2007-05-23 | 北京宝得瑞食品有限公司 | Preparation method of seabuckthorn fruit powder and production equipment thereof |
| CN101178283A (en) * | 2006-11-06 | 2008-05-14 | 谢洪清 | Seasoner sponging drying machine group |
| CN201551860U (en) * | 2009-11-23 | 2010-08-18 | 陆文光 | Centrifugal spray dryer unit |
| CN102374759A (en) * | 2010-08-11 | 2012-03-14 | 焦作健康元生物制品有限公司 | Mushroom scrap spray-drying system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107875661A (en) * | 2017-12-25 | 2018-04-06 | 无锡市尚德干燥设备有限公司 | Multilevel drying machine |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| DD01 | Delivery of document by public notice |
Addressee: Zhu Zheng Document name: Notification of Passing Examination on Formalities |
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| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20140129 |